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CN103820160A - Combustion chamber, coal water slurry gasification furnace with water wall and multiple opposite nozzles, and application of coal water slurry gasification furnace - Google Patents

Combustion chamber, coal water slurry gasification furnace with water wall and multiple opposite nozzles, and application of coal water slurry gasification furnace Download PDF

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Publication number
CN103820160A
CN103820160A CN201410075026.2A CN201410075026A CN103820160A CN 103820160 A CN103820160 A CN 103820160A CN 201410075026 A CN201410075026 A CN 201410075026A CN 103820160 A CN103820160 A CN 103820160A
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combustion chamber
nozzle
coal
water slurry
water wall
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周志杰
梁钦锋
于广锁
刘海峰
龚欣
代正华
陈雪莉
王亦飞
王辅臣
王兴军
郭晓镭
李伟锋
许建良
郭庆华
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East China University of Science and Technology
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Abstract

本发明涉及一种燃烧室及其水冷壁多喷嘴对置式水煤浆气化炉和应用,所述燃烧室包括金属炉壳(1)、盘管式水冷壁内件(2)、设于所述燃烧室顶部的预热喷嘴室(3)、工艺喷嘴室(4)、位于所述燃烧室下端中心部位的气渣出口(5);所述工艺喷嘴室(4)按水平方向分1~3层设置在所述燃烧室的上半部分空间,每一层设有1~3对所述工艺喷嘴室(4);所述盘管式水冷壁内件(2)由2~10根相同规格的金属管盘绕而成,所述金属管的进出端部与集箱连接。本发明设计的燃烧室大大拓展了水煤浆气化工艺的煤种适应范围,其部件可单独更换或维修,安装在多个工艺喷嘴室4内的工艺喷嘴可以全部或者部分工艺喷嘴进行工作,大大增加了气化炉的运行负荷范围。The invention relates to a combustion chamber and its water-cooled wall multi-nozzle opposed coal-water slurry gasification furnace and its application. The preheating nozzle chamber (3) on the top of the combustion chamber, the process nozzle chamber (4), and the gas slag outlet (5) located at the center of the lower end of the combustion chamber; the process nozzle chamber (4) is divided into 1~ 3 layers are arranged in the upper half space of the combustion chamber, and each layer is provided with 1 to 3 pairs of the process nozzle chambers (4); The standard metal pipe is coiled, and the inlet and outlet ends of the metal pipe are connected with the header. The combustion chamber designed by the present invention greatly expands the coal type adaptability range of the coal-water slurry gasification process, its components can be replaced or repaired separately, and the process nozzles installed in a plurality of process nozzle chambers 4 can work in whole or in part. The operating load range of the gasifier is greatly increased.

Description

一种燃烧室及其水冷壁多喷嘴对置式水煤浆气化炉和应用Combustion chamber and its water wall multi-nozzle opposed coal-water slurry gasifier and its application

技术领域technical field

本发明涉及一种燃烧室及其水煤浆气化炉的结构,采用水冷壁作为多喷嘴对置式水煤浆气化炉的内件衬里。The invention relates to a combustion chamber and the structure of a coal-water slurry gasification furnace. A water-cooled wall is used as the internal part lining of the multi-nozzle opposed coal-water slurry gasification furnace.

背景技术Background technique

气流床水煤浆气化技术近年来已经获得广泛应用。其中有代表性的技术包括美国GE公司的水煤浆气化技术(原Texaco水煤浆气化技术)、华东理工大学开发的多喷嘴对置式煤气化技术(中国专利,专利号ZL98110616.1,ZL2005101114824.8,ZL01210097.8)。Entrained bed coal-water slurry gasification technology has been widely used in recent years. Among them, representative technologies include the coal-water slurry gasification technology of GE Company of the United States (formerly Texaco coal-water slurry gasification technology), and the multi-nozzle opposed coal gasification technology developed by East China University of Science and Technology (Chinese patent, patent number ZL98110616.1, ZL2005101114824.8, ZL01210097.8).

传统的气流床水煤浆气化技术一般采用以耐火砖及隔热保温材料作为气化炉燃烧室隔热衬里。这种气化炉燃烧室的衬里形式具有高温保护及蓄热、隔热作用。Traditional entrained bed coal-water slurry gasification technology generally uses refractory bricks and thermal insulation materials as the thermal insulation lining of the combustion chamber of the gasifier. The lining form of the combustion chamber of the gasifier has the functions of high temperature protection, heat storage and heat insulation.

耐火砖形式的燃烧室衬里主要存在以下几点不足:The combustion chamber lining in the form of refractory bricks mainly has the following shortcomings:

1、对水煤浆气化的原料煤有限制。目前,传统的以耐火砖为衬里的水煤浆气化炉,一般采用灰熔融温度较低的烟煤作为气化煤原料。之所以采用灰熔融温度较低的煤,是因为气流床气化炉一般都采用液态排渣的方式,要使煤灰变成液态渣,就需要气化区温度高于灰熔融温度以将煤灰烧熔。但是,气化温度过高,会大大加剧耐火衬里材料的蚀损,为了保证一定的耐火衬里材料使用寿命,就不得不采用灰熔融温度较低的煤,这大大限制了中国广泛存在的高灰融点煤在水煤浆气化工艺中的适用性。1. There are restrictions on raw coal for coal-water slurry gasification. At present, traditional coal-water slurry gasifiers lined with refractory bricks generally use bituminous coal with a low ash melting temperature as the gasification coal raw material. The reason why coal with a lower ash melting temperature is used is that entrained bed gasifiers generally adopt the method of liquid slag removal. To turn coal ash into liquid slag, the temperature in the gasification zone needs to be higher than the ash melting temperature to remove the coal ash. Ashes melted. However, if the gasification temperature is too high, the corrosion of the refractory lining material will be greatly aggravated. In order to ensure a certain service life of the refractory lining material, coal with a lower ash melting temperature has to be used, which greatly limits the high ash that widely exists in China. Applicability of melting point coal in coal water slurry gasification process.

2、耐火砖需要定期更换,费用高,环境问题较大。即使采用适宜的水煤浆气化用煤(指灰熔点较低),耐火砖衬里,尤其是最内层抗高温的耐火砖,由于其受到高温气渣的侵蚀、冲刷,在使用一段时间后,就需要对局部或者整体耐火砖衬里进行更换。这一方面增加了企业的运行成本,另外,由于目前的耐火砖材料基本采用铬作为主要原料,而铬的制备熔融等过程带来严重的环境问题。2. Refractory bricks need to be replaced regularly, which leads to high costs and serious environmental problems. Even if suitable coal for coal-water slurry gasification (referring to low melting point of ash), the refractory brick lining, especially the innermost high-temperature resistant refractory brick, will be damaged after a period of use due to the erosion and erosion of high-temperature gas slag. , it is necessary to replace the partial or overall refractory brick lining. On the one hand, this increases the operating cost of the enterprise. In addition, since the current refractory brick materials basically use chromium as the main raw material, the preparation and melting of chromium brings serious environmental problems.

耐火砖需要预热,增加了运行成本,减少了设备可利用率。Refractory bricks need to be preheated, which increases operating costs and reduces equipment availability.

发明内容Contents of the invention

本发明的主要目的是提供一种以水冷壁为水煤浆气化炉燃烧室衬里的技术,以解决传统的以耐火砖为衬里的水煤浆气化炉燃烧室存在的弊端。The main purpose of the present invention is to provide a kind of technology that uses water wall as the combustion chamber lining of coal-water slurry gasifier to solve the disadvantages of the traditional combustion chamber of coal-water slurry gasifier that uses refractory bricks as the lining.

一种燃烧室,所述燃烧室包括金属炉壳1、盘管式水冷壁内件2、设于所述燃烧室顶部的预热喷嘴室3、工艺喷嘴室4、位于所述燃烧室下端中心部位的气渣出口5;A combustion chamber, which includes a metal furnace shell 1, a coiled water-cooled wall inner part 2, a preheating nozzle chamber 3 arranged on the top of the combustion chamber, a process nozzle chamber 4, and a center of the lower end of the combustion chamber Part of the air slag outlet 5;

所述工艺喷嘴室4按水平方向分1~3层(每一层的工艺喷嘴室4位于同一水平面)设置在所述燃烧室的上半部分空间,每一层设有1~3对所述工艺喷嘴室4,且每一层的所述工艺喷嘴室4在所述气化炉的圆周方向上均匀布置;The process nozzle chamber 4 is divided into 1 to 3 layers in the horizontal direction (the process nozzle chamber 4 of each layer is located on the same horizontal plane) and is arranged in the upper half space of the combustion chamber, and each layer is provided with 1 to 3 pairs of the Process nozzle chambers 4, and the process nozzle chambers 4 of each layer are evenly arranged in the circumferential direction of the gasifier;

所述盘管式水冷壁内件2由2~10根相同规格的金属管盘绕而成,所述金属管的进出端部与集箱连接;所述盘管式水冷壁内件2的竖直轴线与所述金属炉壳1的竖直轴线重合;The coil-type water-cooled wall internals 2 are coiled from 2 to 10 metal tubes of the same specification, and the inlet and outlet ends of the metal tubes are connected to the header; the vertical coil-type water-cooled wall internals 2 The axis coincides with the vertical axis of the metal furnace shell 1;

所述气渣出口5与所述燃烧室在竖直方向上同轴,并且,所述气渣出口5由1~5根金属管盘绕而成。The gas slag outlet 5 is coaxial with the combustion chamber in the vertical direction, and the gas slag outlet 5 is formed by coiling 1 to 5 metal pipes.

所述预热喷嘴室3与所述金属炉壳1的竖直轴线重合,并且,所述预热喷嘴室3由1~5根金属管盘绕而成。The preheating nozzle chamber 3 coincides with the vertical axis of the metal furnace shell 1, and the preheating nozzle chamber 3 is formed by coiling 1 to 5 metal pipes.

所述预热喷嘴室3与所述盘管式水冷壁内件2之间具有用弹性轻质耐火材料填充的缝隙。There is a gap filled with elastic light refractory material between the preheating nozzle chamber 3 and the coiled water-cooled wall inner part 2 .

所述气渣出口5与所述盘管式水冷壁内件2之间具有用弹性轻质耐火材料填充的缝隙。There is a gap filled with elastic light refractory material between the gas slag outlet 5 and the coiled water-cooled wall inner part 2 .

所述工艺喷嘴室4包括所述金属炉壳1的炉壳水平孔6和所述盘管式水冷壁内件2的水冷壁水平孔7,所述炉壳水平孔6与所述水冷壁水平孔7之间通过波纹管9互相联接,所述炉壳水平孔6、水冷壁水平孔7的水平中心轴线互相平行。The process nozzle chamber 4 includes the furnace shell horizontal hole 6 of the metal furnace shell 1 and the water-cooled wall horizontal hole 7 of the coiled water-cooled wall internal part 2, and the furnace shell horizontal hole 6 is horizontal to the water-cooled wall The holes 7 are connected to each other by bellows 9, and the horizontal central axes of the horizontal holes 6 of the furnace shell and the horizontal holes 7 of the water cooling wall are parallel to each other.

一种水冷壁多喷嘴对置式水煤浆气化炉,具有以上任一所述的燃烧室。A water-cooled wall multi-nozzle opposed coal-water slurry gasifier has any one of the above-mentioned combustion chambers.

上述水冷壁多喷嘴对置式水煤浆气化炉的应用,具体为:将所述气化炉用于水煤浆进料气流床的气化,包括如下步骤:通过安装于工艺喷嘴室4的工艺喷嘴将水煤浆气化原料和氧气喷入所述燃烧室,进行气化反应,生成的高温气体及高温熔渣向下流动,经过所述气渣出口5排出所述燃烧室。The application of the above-mentioned multi-nozzle opposed coal-water slurry gasifier with a water wall is specifically: using the gasifier for the gasification of the coal-water slurry feed entrained flow bed, including the following steps: The process nozzle sprays coal-water slurry gasification raw materials and oxygen into the combustion chamber for gasification reaction, and the generated high-temperature gas and high-temperature slag flow downward and are discharged from the combustion chamber through the gas slag outlet 5 .

在所述气化反应的初期,通过所述预热喷嘴室3内安装的预热喷嘴喷入气态或液态的燃料和氧化剂(例如,空气等),进行燃烧反应,使所述盘管式水冷壁内件2进行预热;当所述盘管式水冷壁内件2预热到指定温度时,再将所述水煤浆气化原料和所述氧气通过安装于工艺喷嘴室4的工艺喷嘴喷入所述燃烧室并由所述预热喷嘴的火焰点燃;待所述工艺喷嘴的火焰稳定后,熄灭所述预热喷嘴的火焰。In the initial stage of the gasification reaction, gaseous or liquid fuel and oxidant (for example, air, etc.) are sprayed into the preheating nozzle installed in the preheating nozzle chamber 3 to carry out the combustion reaction, and the coiled water cooling The wall internals 2 are preheated; when the coil-type water-cooled wall internals 2 are preheated to a specified temperature, the coal-water slurry gasification raw material and the oxygen are passed through the process nozzle installed in the process nozzle chamber 4 spray into the combustion chamber and be ignited by the flame of the preheating nozzle; after the flame of the process nozzle is stable, extinguish the flame of the preheating nozzle.

在所述工艺喷嘴全部或者部分已经建立起与所述水煤浆气化原料和氧气的稳定火焰,并熄灭所述预热喷嘴的火焰后,继续通入氮气、二氧化碳、水蒸汽中的单一或混合气体,或者继续通入新的水煤浆气化原料和氧气作为气化进料,或者通入气化反应所产生的混合气;After all or part of the process nozzle has established a stable flame with the coal-water slurry gasification raw material and oxygen, and extinguished the flame of the preheating nozzle, continue to feed nitrogen, carbon dioxide, steam or Mixed gas, or continue to feed new coal-water slurry gasification raw materials and oxygen as gasification feed, or feed mixed gas generated by gasification reaction;

其中,当所述工艺喷嘴的部分喷入所述水煤浆气化原料和氧气进行气化反应时,所述工艺喷嘴的其他部分喷入少量氮气、二氧化碳、水蒸汽中的单一或者混合气体,以保护工艺喷嘴不被气化反应形成的高温所损坏。Wherein, when part of the process nozzle is injected into the coal-water slurry gasification raw material and oxygen for gasification reaction, other parts of the process nozzle are injected with a small amount of single or mixed gases in nitrogen, carbon dioxide, and water vapor, To protect the process nozzle from being damaged by the high temperature formed by the gasification reaction.

与传统的以耐火砖为衬里的水煤浆气化技术相比,本发明具有以下显著优点:Compared with the traditional coal-water slurry gasification technology lined with refractory bricks, the present invention has the following significant advantages:

1、采用水冷壁作为水煤浆气化炉内部结构,利用水冷壁“以渣抗渣”的特点,可气化灰熔融温度较高的煤,大大拓展了水煤气化工艺的煤种适应范围。1. The water-cooled wall is used as the internal structure of the coal-water slurry gasifier, and the characteristics of "resisting slag with slag" of the water-cooled wall can be used to gasify coal with a high ash melting temperature, which greatly expands the coal type application range of the water-coal gasification process.

2、采用盘管式水冷壁2作为气化炉燃烧室主体内部结构,顶部的预热喷嘴室3、侧置的工艺喷嘴室4及下部的气渣出口5与盘管式水冷壁之间不直接固定连接,间隙处用弹性轻质耐火材料填充。这样,后三者都可以与盘管式水冷壁脱离,单独更换或维修。一方面提高了相关部件的使用可靠性,另一方面也最大程度降低了水冷壁主体的故障率和维修工作量。2. The coil-type water-cooled wall 2 is used as the main internal structure of the combustion chamber of the gasifier. There is no gap between the top preheating nozzle chamber 3, the side-mounted process nozzle chamber 4 and the lower gas slag outlet 5 and the coil-type water-cooled wall. The connection is directly fixed, and the gap is filled with elastic lightweight refractory material. In this way, the latter three can be separated from the coil water cooling wall, and can be replaced or repaired separately. On the one hand, it improves the reliability of related components, and on the other hand, it also minimizes the failure rate and maintenance workload of the main body of the water-cooled wall.

3、采用安装在顶部预热喷嘴室3内的预热喷嘴对气化炉燃烧室内部进行预热,并提供稳定火焰点燃安装在工艺喷嘴室4内的工艺喷嘴喷入的煤浆和氧气,不需要在同一个喷嘴内进行预燃火焰和煤浆氧气工艺进料的切换,使得水煤浆气化炉开车过程简单可靠。3. Use the preheating nozzle installed in the top preheating nozzle chamber 3 to preheat the inside of the combustion chamber of the gasifier, and provide a stable flame to ignite the coal slurry and oxygen injected by the process nozzle installed in the process nozzle chamber 4, There is no need to switch the pre-combustion flame and the coal slurry oxygen process feed in the same nozzle, which makes the start-up process of the coal-water slurry gasifier simple and reliable.

4、安装在多个工艺喷嘴室4内的工艺喷嘴,可以全部或者部分工艺喷嘴进行工作,大大增加了气化炉的运行负荷范围。4. The process nozzles installed in multiple process nozzle chambers 4 can work with all or part of the process nozzles, which greatly increases the operating load range of the gasifier.

附图说明Description of drawings

图1是水冷壁多喷嘴对置式水煤浆气化炉中燃烧室的结构示意图;Fig. 1 is the structural representation of the combustion chamber in the multi-nozzle opposed type coal-water slurry gasifier with water wall;

图2是盘管式水冷壁内件的结构示意图。Fig. 2 is a structural schematic diagram of the inner part of the coiled water-cooled wall.

符号说明:Symbol Description:

1金属炉壳;2盘管式水冷壁内件;3预热喷嘴室;4工艺喷嘴室;1 Metal furnace shell; 2 Coil water-cooled wall internals; 3 Preheating nozzle chamber; 4 Process nozzle chamber;

5气渣出口;6炉壳水平孔;7水冷壁水平孔,8工艺喷嘴;5 gas slag outlet; 6 horizontal hole in the furnace shell; 7 horizontal hole in the water wall, 8 process nozzle;

9波纹管;10定位块;11水冷壁盘管进水管;9 bellows; 10 positioning block; 11 water wall coil inlet pipe;

12水冷壁盘管出水管;13预热喷嘴;14弹性轻质耐火材料;12 water wall coil outlet pipe; 13 preheating nozzle; 14 elastic light refractory material;

15预热喷嘴开口;16气渣出口开口。15 preheating nozzle opening; 16 air slag outlet opening.

具体实施方式Detailed ways

下面将结合实施例进一步阐明本发明的内容,但这些实施例并不限制本发明的保护范围。The content of the present invention will be further illustrated below in conjunction with examples, but these examples do not limit the protection scope of the present invention.

实施例1Example 1

如图1所示,水冷壁多喷嘴对置式水煤浆气化炉中燃烧室具有金属炉壳1,其主体为筒状结构,金属炉壳1的上部为一球形封头、下部为圆锥状结构。该金属炉壳1的下部可联接一个同径或者异径的气化洗涤冷却设备或者热回收设备。球形封头中心、筒体直段及圆锥状下部的下端设置圆形开口,以分别作为预热喷嘴13、工艺喷嘴8及气渣出口5的安装位置。As shown in Figure 1, the combustion chamber in the water-wall multi-nozzle opposed coal-water slurry gasifier has a metal furnace shell 1, the main body of which is a cylindrical structure. The upper part of the metal furnace shell 1 is a spherical head and the lower part is conical. structure. The lower part of the metal furnace shell 1 can be connected with a gasification washing cooling device or heat recovery device with the same diameter or different diameter. The center of the spherical head, the straight section of the cylinder and the lower end of the conical lower part are provided with circular openings, which are respectively used as installation positions for the preheating nozzle 13, the process nozzle 8 and the gas slag outlet 5.

燃烧室还具有盘管式水冷壁内件2、设于燃烧室顶部的预热喷嘴室3、工艺喷嘴室4、位于燃烧室下端中心部位的气渣出口5。The combustion chamber also has a coil-type water-cooled wall internal part 2, a preheating nozzle chamber 3 located on the top of the combustion chamber, a process nozzle chamber 4, and an air slag outlet 5 located at the center of the lower end of the combustion chamber.

为了确保热胀冷缩过程中盘管式水冷壁内件2与金属炉壳1之间保持一定距离,设置了定位块10。In order to ensure a certain distance between the coiled water-cooled wall inner part 2 and the metal furnace shell 1 during thermal expansion and contraction, a positioning block 10 is provided.

工艺喷嘴室4按水平方向分1~3层设置在燃烧室的上半部分空间,每一层设有1~3对工艺喷嘴室4,即,同一层的工艺喷嘴室4位于同一水平面,且同一层的工艺喷嘴室4在气化炉的圆周方向上均匀布置;The process nozzle chamber 4 is arranged in the upper half space of the combustion chamber in 1 to 3 layers in the horizontal direction, and each layer is provided with 1 to 3 pairs of process nozzle chambers 4, that is, the process nozzle chambers 4 on the same layer are located on the same horizontal plane, and The process nozzle chambers 4 on the same layer are evenly arranged in the circumferential direction of the gasifier;

气渣出口5与燃烧室在竖直方向上同轴,由1~5根金属管盘绕而成。The gas slag outlet 5 is coaxial with the combustion chamber in the vertical direction, and is formed by coiling 1 to 5 metal pipes.

预热喷嘴室3与金属炉壳1的竖直轴线重合,由1~5根金属管盘绕而成。预热喷嘴室3设置在燃烧室顶部中心处,由一个独立可拆卸的由金属管盘绕而成的筒形结构并以同轴的方式安装于盘管式水冷壁内件2顶部开口空间内形成。采用本发明设计的预热喷嘴室3结构,可以独立更换检修预热喷嘴室,而不影响主体水冷壁盘管。The preheating nozzle chamber 3 coincides with the vertical axis of the metal furnace shell 1 and is formed by coiling 1 to 5 metal tubes. The preheating nozzle chamber 3 is arranged at the center of the top of the combustion chamber, and is formed by an independent and detachable cylindrical structure coiled by a metal tube and coaxially installed in the open space at the top of the coiled water-cooled wall internal part 2 . Adopting the structure of the preheating nozzle chamber 3 designed by the present invention, the preheating nozzle chamber can be replaced and repaired independently without affecting the main water wall coil.

预热喷嘴室3与盘管式水冷壁内件2之间以及气渣出口5与盘管式水冷壁内件2之间具有用弹性轻质耐火材料14填充的缝隙(3~200mm)。There are gaps (3-200 mm) filled with elastic light refractory material 14 between the preheating nozzle chamber 3 and the coiled water-cooled wall inner part 2 and between the air slag outlet 5 and the coiled water-cooled wall inner part 2 .

工艺喷嘴室4包括金属炉壳1的炉壳水平孔6和盘管式水冷壁内件2的水冷壁水平孔7,炉壳水平孔6与水冷壁水平孔7之间通过波纹管9互相联接,炉壳水平孔6、水冷壁水平孔7的水平中心轴线互相平行。The process nozzle chamber 4 includes the furnace shell horizontal hole 6 of the metal furnace shell 1 and the water-cooled wall horizontal hole 7 of the coil-type water-cooled wall inner part 2, and the furnace shell horizontal hole 6 and the water-cooled wall horizontal hole 7 are connected to each other by a bellows 9 , the horizontal central axes of the furnace shell horizontal hole 6 and the water wall horizontal hole 7 are parallel to each other.

工艺喷嘴室4设计在燃烧室直段的侧面,如前所述,在与金属炉壳1和水冷壁盘管2相对应的位置上均有开口空间,在开口空间内形成由一个独立可拆卸的由金属管盘绕而成的筒形结构,该筒形结构为与水冷壁盘管2开口的中心轴平行的工艺喷嘴室内筒。但是,在冷态安装时,工艺喷嘴室内筒的中心轴略低于水冷壁盘管2开口的中心轴,这是考虑盘管式水冷壁内件2在热态状态下膨胀后,其开口中心轴与内筒中心轴尽量共轴。工艺喷嘴室内筒在靠近金属炉壳1一侧与波纹管9及一个同径短接管固定,短接管通过焊接的方式固定在金属炉壳1上。通过波纹管9,可消除由于热胀冷缩效应造成的工艺喷嘴室内筒与其固定端之间的应力。工艺喷嘴室内筒与主体水冷壁盘管之间预留一定的间隙(3~200mm),间隙空间内用弹性轻质耐火材料填充。工艺喷嘴室内筒可独立拆卸检修,而不影响主体水冷壁盘管。The process nozzle chamber 4 is designed on the side of the straight section of the combustion chamber. As mentioned above, there is an open space at the position corresponding to the metal furnace shell 1 and the water-cooled wall coil 2, and an independent detachable nozzle is formed in the open space. A cylindrical structure formed of coiled metal tubes, the cylindrical structure is an indoor cylinder of the process nozzle parallel to the central axis of the opening of the water wall coil 2 . However, when installed in a cold state, the central axis of the inner cylinder of the process nozzle is slightly lower than the central axis of the opening of the water-cooled wall coil 2. The shaft and the central axis of the inner cylinder are as coaxial as possible. The inner tube of the process nozzle is fixed on the side close to the metal furnace shell 1 with the bellows 9 and a short connection pipe with the same diameter, and the short connection pipe is fixed on the metal furnace shell 1 by welding. The bellows 9 can eliminate the stress between the inner cylinder of the process nozzle and its fixed end caused by thermal expansion and contraction. A certain gap (3-200mm) is reserved between the inner cylinder of the process nozzle and the main water-cooled wall coil, and the gap space is filled with elastic light-weight refractory materials. The inner barrel of the process nozzle can be disassembled and repaired independently without affecting the main water wall coil.

气渣出口5位于盘管式水冷壁内件2下部锥底中心处。气渣出口5由一个独立可拆卸的由金属管盘绕而成的筒形结构形成气渣出口内筒,气渣出口内筒与盘管式水冷壁内件2下部的气渣出口5的开口空间同轴,且有一定的间隙(3~200mm),间隙空间内用弹性轻质耐火材料填充。气渣出口内筒可独立拆卸检修,而不影响盘管式水冷壁内件2。The air slag outlet 5 is located at the center of the cone bottom at the lower part of the coil-type water-cooled wall inner part 2 . The air slag outlet 5 is formed by an independent and detachable cylindrical structure coiled by a metal tube to form the air slag outlet inner cylinder, and the opening space between the air slag outlet inner cylinder and the air slag outlet 5 at the lower part of the coiled water wall internal part 2 Coaxial, and have a certain gap (3 ~ 200mm), the gap space is filled with elastic light refractory material. The air slag outlet inner cylinder can be disassembled and repaired independently without affecting the inner part 2 of the coiled water cooling wall.

如图2所示的盘管式水冷壁内件,其主体为一个盘管式结构。所谓盘管式,是若干根(本发明为2~10根,优选3~5根)金属管平行螺旋盘绕而成,并在相应的位置留出预热喷嘴室3、工艺喷嘴室4及气渣出口5的开口空间(图中示出了预热喷嘴开口15和气渣出口开口16)。为了保护金属盘管,可在靠近炉膛一侧的金属盘管表面敷设一层0.5~200mm厚的隔热耐火材料,如碳化硅。当气化炉燃烧室内发生水煤浆气化反应过程时,煤中的灰渣在高温下熔融,部分灰渣粘附到水冷壁表面后被冷却固化,从而形成一个动态保护层,以保护水冷壁盘管不被高温烧蚀。这一动态渣层随着煤种和气化温度的不同而发生厚度的改变,但总体上,从水冷壁盘管壁面向炉膛内依次为:固态渣层、软化渣层和流动渣层。As shown in Fig. 2, the coil type water-cooled wall inner part has a main body of a coil type structure. The so-called coiled tube type is formed by a number of metal tubes (2 to 10 in the present invention, preferably 3 to 5) that are spirally coiled in parallel, and the preheating nozzle chamber 3, the process nozzle chamber 4 and the gas nozzle chamber 4 are reserved at corresponding positions. The opening space of the slag outlet 5 (preheating nozzle opening 15 and gas slag outlet opening 16 are shown in the figure). In order to protect the metal coil, a layer of 0.5-200mm thick heat-insulating refractory material, such as silicon carbide, can be laid on the surface of the metal coil near the furnace. When the coal-water slurry gasification reaction process occurs in the combustion chamber of the gasifier, the ash in the coal melts at high temperature, and part of the ash adheres to the surface of the water wall and is cooled and solidified, thereby forming a dynamic protective layer to protect the water cooling wall. The wall coil is not ablated by high temperature. The thickness of this dynamic slag layer changes with the coal type and gasification temperature, but in general, from the wall of the water-cooled wall coil to the furnace, the order is: solid slag layer, softened slag layer and mobile slag layer.

平行螺旋盘绕的金属管的进出端部与集箱连接;盘管式水冷壁内件2的竖直轴线与所述金属炉壳1的竖直轴线重合,具有水冷壁盘管进水管11和水冷壁盘管出水管12。The inlet and outlet ends of parallel helically coiled metal pipes are connected to the header; the vertical axis of the coiled water-cooled wall internal part 2 coincides with the vertical axis of the metal furnace shell 1, and has a water-cooled wall coil inlet pipe 11 and a water-cooled Wall coil pipe outlet pipe 12.

按照本发明设计的气化炉燃烧室,具有开工点火快捷稳定的特点。通过设置在顶部的预热喷嘴室内的预热喷嘴,用柴油、天然气、液化气、工厂驰放气或者其他气液态燃料,与空气进行燃烧反应,首先对主体水冷壁盘管进行预热,然后通过设置在工艺喷嘴室内的工艺喷嘴,喷入水煤浆和氧气,被预热喷嘴形成的火焰所点燃,进行气化燃烧反应,预热喷嘴火焰可维持一段时间,待工艺喷嘴火焰完全稳定后再熄灭。火焰熄灭后的预热喷嘴可喷入少量氮气、二氧化碳或者蒸汽等气体对自身进行保护。由于本发明设计的气化炉燃烧室设有多个工艺喷嘴室及其工艺喷嘴,在系统进行投料工作时,可以一对喷嘴投料,也可以两对喷嘴同时投料。The combustion chamber of the gasification furnace designed according to the invention has the characteristics of fast and stable ignition at start-up. Through the preheating nozzle in the preheating nozzle chamber on the top, diesel, natural gas, liquefied petroleum gas, factory bleed gas or other gas and liquid fuels are used for combustion reaction with air. First, the main water-cooled wall coil is preheated, and then The coal-water slurry and oxygen are sprayed through the process nozzle installed in the process nozzle chamber, ignited by the flame formed by the preheating nozzle, and the gasification combustion reaction is carried out. The flame of the preheating nozzle can be maintained for a period of time. After the flame of the process nozzle is completely stable, off. After the flame is extinguished, the preheating nozzle can inject a small amount of nitrogen, carbon dioxide or steam to protect itself. Since the combustion chamber of the gasification furnace designed by the present invention is provided with a plurality of process nozzle chambers and process nozzles, when the system is feeding materials, one pair of nozzles can feed materials, or two pairs of nozzles can feed materials at the same time.

按照本发明设计的气化炉燃烧室,还具有负荷范围宽,调节手段灵活的特点。由于设置了多个工艺喷嘴室及其工艺喷嘴,气化炉燃烧室可以采用所有工艺喷嘴以相同的负荷工作,也可以部分工艺喷嘴工作而其他工艺喷嘴在用少量氮气、二氧化碳或者蒸汽保护的情况下可以停止工作,或者不同位置的工艺喷嘴按照不同负荷工作,通过这些灵活调节手段,可以使整体气化炉在极大的负荷范围内工作。The combustion chamber of the gasification furnace designed according to the invention also has the characteristics of wide load range and flexible adjustment means. Due to the setting of multiple process nozzle chambers and their process nozzles, the combustion chamber of the gasifier can use all process nozzles to work at the same load, or some process nozzles can work while other process nozzles are protected with a small amount of nitrogen, carbon dioxide or steam The gasifier can be stopped working under different conditions, or the process nozzles in different positions work according to different loads. Through these flexible adjustment methods, the overall gasifier can work within a very large load range.

Claims (10)

1. a combustion chamber, it is characterized in that, described combustion chamber comprises metal furnace shell (1), coil tube type water wall internals (2), is located at the preheating nozzle box (3) of described top of combustion chamber, technique nozzle box (4), be positioned at the gas slag outlet (5) in centre, lower end, described combustion chamber;
Described technique nozzle box (4) divides 1~3 layer of upper part space that is arranged on described combustion chamber by horizontal direction, every one deck is provided with 1~3 pair of described technique nozzle box (4), and the described technique nozzle box (4) of every one deck is evenly arranged on the circumferential direction of described vapourizing furnace;
Described coil tube type water wall internals (2) are coiled to form by the metal tube of 2~10 same sizes, and the turnover end of described metal tube is connected with header; The vertical axis of described coil tube type water wall internals (2) overlaps with the vertical axis of described metal furnace shell (1).
2. combustion chamber according to claim 1, is characterized in that, described gas slag outlet (5) is coaxial with described combustion chamber in the vertical direction, and described gas slag outlet (5) is coiled to form by 1~5 metal tube.
3. combustion chamber according to claim 1, is characterized in that, described preheating nozzle box (3) overlaps with the vertical axis of described metal furnace shell (1), and described preheating nozzle box (3) is coiled to form by 1~5 metal tube.
4. combustion chamber according to claim 1, is characterized in that, has the gap of filling with elastomeric light fire resistant materials between described preheating nozzle box (3) and described coil tube type water wall internals (2).
5. combustion chamber according to claim 1, is characterized in that, has the gap of filling with elastomeric light fire resistant materials between described gas slag outlet (5) and described coil tube type water wall internals (2).
6. combustion chamber according to claim 1, it is characterized in that, described technique nozzle box (4) comprises the furnace shell lateral aperture (6) of described metal furnace shell (1) and the water wall lateral aperture (7) of described coil tube type water wall internals (2), between described furnace shell lateral aperture (6) and described water wall lateral aperture (7), connect mutually by corrugated tube (9), the horizontal center line axis of described furnace shell lateral aperture (6), water wall lateral aperture (7) is parallel to each other.
7. a water wall multiple-nozzle contraposition type coal water slurry gasification stove, is characterized in that, the described gasification stove arbitrary described combustion chamber of requirement 1 to 6 of having the right.
8. the application of water wall multiple-nozzle contraposition type coal water slurry gasification stove claimed in claim 7, it is characterized in that, gasification by described vapourizing furnace for coal water slurry feeding gas fluidized bed, comprise the steps: that coal water slurry gasification raw material and oxygen are sprayed into described combustion chamber by the technique nozzle by being installed on technique nozzle box (4), carry out gasification reaction, the high-temperature gas and the high-temperature slag that generate flow downward, and discharge described combustion chamber through described gas slag outlet (5).
9. application according to claim 8, it is characterized in that, at the initial stage of described gasification reaction, spray into gaseous state or liquid fuel and oxygenant by the pre-hot nozzle of installing in described preheating nozzle box (3), carry out combustion reactions, make described coil tube type water wall internals (2) carry out preheating; In the time that described coil tube type water wall internals (2) are preheating to assigned temperature, more described coal water slurry gasification raw material and described oxygen are sprayed into described combustion chamber the flame ignition by described pre-hot nozzle by being installed on the technique nozzle of technique nozzle box (4); After the flame stabilization of described technique nozzle, extinguish the flame of described pre-hot nozzle.
10. application according to claim 9, it is characterized in that, set up in whole or in part and the stationary flame of described coal water slurry gasification raw material and oxygen at described technique nozzle, and extinguish after the flame of described pre-hot nozzle, continue to pass into the single or mixed gas in nitrogen, carbonic acid gas, water vapor, or continue to pass into new coal water slurry gasification raw material and oxygen as gasification feed, or pass into the gas mixture that gasification reaction produces;
Wherein, in the time that the part of described technique nozzle sprays into described coal water slurry gasification raw material and oxygen and carries out gasification reaction, other parts of described technique nozzle spray into the single or mixed gas in a small amount of nitrogen, carbonic acid gas, water vapor.
CN201410075026.2A 2014-03-03 2014-03-03 Combustion chamber, coal water slurry gasification furnace with water wall and multiple opposite nozzles, and application of coal water slurry gasification furnace Pending CN103820160A (en)

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Application publication date: 20140528